南水北调丹江口水库原水有机物分子组成规律及其强化混凝处理的效能对比

以取自南水北调中线工程的丹江口水库原水作为研究对象,考察了丹江口水库原水中有机物的分子量大小和亲疏水性分子组成规律,并确定了其所适用的强化混凝工艺条件.分离试验表明,丹江口原水中有机物主要以小分子量形式存在.其中,1 000组分的溶解性有机碳(DOC)和UV254所占比例最大,分别为39.98%和39.10%,且此区间还具有最高的三卤甲烷生成潜能(THMFP)和含氮消毒副产物生成潜能(N-DBPFP).亲疏水性方面,原水中弱疏水性组分含量最高,疏水性有机物的比例用DOC表征时超过80%.强疏水性组分含量最低但是强疏水性组分的THMFP最大,占总量的57.31%,而各组分的NDBPFP则相差不大.混凝试验表明,当采用聚合硫酸铁(PFS,4 mg·L-1)和聚丙烯酰胺(PAM,0.4 mg·L-1)处理丹江口原水时,强化混凝效果最好,可实现较为有效的去除浊度(76.33%)、DOC(25.57%)、UV254(37.78%)及THMFP(23.16%).本研究成果可为南水北调河南受水区既有水厂升级改造与工艺的优化运行提供有效的理论和技术支持.     

东江水源水中有机物分子量分布特征研究

采用超滤膜法考察了东江水源水中有机物分子量分布特点,研究了东江泄洪和不泄洪水源水中有机物分子量分布的变化特征。结果表明,东江水源水在不泄洪期间水源水中的溶解性有机物主要为小分子量的有机物。而在泄洪期间,东江水源水中溶解性有机物主要为大分子量的有机物。UV254的分布和有机物分子量分布一致,DOC与UV254具有良好的相关性。泄洪期间水源水中SUVA值小于3,水体中有机物很难通过常规混凝工艺去除,此结果与水厂的实际运行情况相吻合。     

臭氧-生物活性炭对有机物分子量分布的影响

测定了南方某水厂中试规模的臭氧-生物活性炭工艺不同处理阶段(原水、沉淀水、砂滤水、臭氧化水、生物活性炭出水)有机物(TOC和UV254)的分子量(MW)分布.分析了原水中生物可同化有机碳(AOC)的分子量分布.结果表明,AOC主要属于天然有机物(NOM)中MW<1kDa的部分.MW<1kDa的部分占可溶解性有机碳(DOC)的53%～67%,而AOC只占DOC的2.65%～5.91%,表明去除大部分DOC的臭氧-生物活性炭工艺并不能有效去除AOC.     

生物滤池和常规工艺对某地表水中不同分子量有机物的去除

采用生物滤池和常规处理对受污染的某地表水进行试验研究 ,用膜过滤法对其出水进行了分子量分析 ,考察了 2个处理单元对不同分子量区间有机物的去除效果。结果表明 :原水中分子量小于 1 0 0 0的有机物占总 DOC的 78.2 9% ;生物滤池对分子量小于50 0、50 0～ 1 0 0 0和 >60 0 0 0的有机物去除率分别为 54.9%、36.1 %和 2 0 .7% ;常规处理对以上分子量区间有机物的去除率分别为1 5.3%、- 2 0 %和 48.75%。     

生活垃圾焚烧厂贮坑沥滤液的污染与可处理特性

通过对生活垃圾焚烧厂贮坑沥滤液历时6个月的常规污染物监测,分析了沥滤液中溶解性有机物(DOM)分子量分级和重金属在不同分子量DOM中的分布,以探讨沥滤液的污染与可处理特性结果表明:沥滤液有机污染程度高.沥滤液中有机物以非溶解性(约占有机物总量的23%)和分子量＜4 ku的DOM(超过DOM总量的88%)为主,低碳有机酸和醇的总量占沥滤液中DOM(分子量＜4 ku)的50%.沥滤液中重金属含量高,在DOM各分子量分级中,重金属主要与分子量＜4 ku的DOM相关,尤其是Zn和Ni的分布占90%以上,并且重金属(除As和Hg外)的分布与有机物的分布呈显著的正相关性.根据沥滤液的性质,宜采用混凝或厌氧-好氧生物方法对其进行处理.      

废水处理系统中有机物分子量分布及其变化

采用超滤膜法对废水处理系统中有机物的分子量分布及其变化进行研究,分析有机物分子量分布特性及不同分子量分布区间有机物的相对含量。结果表明:厌氧、缺氧、好氧反应池出水中,小于1K分子量区间上的有机物所占比例最高。该分子量区间有机物TOC分别占总TOC的60.9%、58.5%、65.2%,UV254分别占总UV254的69.9%、67.9%、82.1%。传统工艺对小分子量有机物去除效率较低。     

磁性离子交换树脂对原水中有机物去除效能的研究

采用磁性离子交换树脂(MIEX)预处理原水中有机物的中试试验结果表明,MIEX技术可有效地去除原水中的有机物,对UV254,DOC和CODMn的去除率分别稳定在82%、66%和50%,MIEX预处理可以有效强化混凝沉淀对有机物、藻细胞和浊度的去除.与常规工艺相比,在混凝剂聚合氯化铝投加量降低56%时,该工艺对UV254和CODMn的去除率分别为90%和71%,对藻细胞数和浊度的去除率分别为99%和95%.对溶解性有机物分级和分子量分布的测定表明,MIEX预处理主要去除混凝沉淀无法有效去除的小分子区间的亲水性和疏水性有机物,可以有效控制消毒副产物的产生,MIEX预处理与混凝沉淀联用工艺出水的三卤甲烷生成势(THMFP)和卤乙酸生成势(HAAFP)比原水降低了88%和87%.     

水源水消毒副产物生成势与UV254/DOC的相关性研究

使用XAD-4和XAD-8树脂对宜兴3个水源原水中DOM进行亲疏水性分类,采用优化方法测定分类水样的DBPFP,并进行DBPFP与DOM量化指标之间的相关性分析,以确定实际生产过程DBPs生成量的主要影响因素.由三维荧光光谱图得到3个水源原水DOM组成差异较大,水质区别明显.由亲疏水性分类分析发现原水中疏水性和亲水性DOM含量较高,疏水性DOM水样的DBPFP大于原水,得到水样的DBPFP主要取决于DOM与消毒剂反应产生DBPs的效率,而不是DOM的量.引入UV_(254)/DOC这个指标,发现不同分类水样UV_(254)/DOC的差异情况与其DBPFP相吻合,对两者进行回归分析,发现水样THMFP和DHAAFP与UV_(254)/DOC之间存在明显的线性关系,线性可决系数R2分别为0.89和0.85.因此研究减小原水UV_(254)/DOC的技术工艺对于控制给水中DBPs浓度具有重要意义.     

生物预处理对微污染地表水中有机物的去除

采用膜过滤法对某江水、生物滤池出水和常规处理出水进行了分子量分析 ,考察了 2个单元对不同分子量区间有机物的去除率。结果表明 :原水中分子量小于 1K的有机物占总DOC的 80 % ;生物滤池对分子量小于 0 .5K、0 .5～ 1K及 >60K的有机物去除率分别为 2 7.2 %、2 6 .9%和 1 6 .3% ;常规处理对以上分子量区间有机物的去除率分别为 39.2 %、30 .3 %和 2 9.6 %。     

原水碳源分子量分布及DPB效能对酸化时间的响应

采用超滤-纳滤膜法对污水中碳源分子量(MW)进行切割试验,并测定各区间总有机碳(TOC)浓度以了解污水碳源组成特性;同时采用污水酸化技术,研究在不同酸化时间,碳源分子量分布的变化及对厌氧-膜好氧-反硝化(A2N)工艺中反硝化聚磷菌(DPB)用碳和净污效能的影响.结果表明,试验原水TOC为(58.3±2.83) mg /L,其中颗粒有机碳(POC)为(38.05±1.65)mg /L,占65.27%,剩余溶解有机碳(DOC)在分子量0.5kDa以上区间呈现“W”型分布,其中 MW>100kDa、10k~5kDa、1k~0.5kDa、MW<0.5kDa区间碳源分别占36.20%、12.05%、13.68%和29.83%.在不同酸化时间下,POC含量与DOC分布存在显著差异,在12h内酸化,可以有效将POC转化为DOC,且在14mg/L左右趋于平衡;DOC在大于0.5kDa区间上的分布呈现随时间而整体后移的趋势,在8h时碳源质量最优,其中MW<1kDa的小分子有机物高达17.30mg/L;此时,DPB污泥在厌氧池与缺氧池中的碳源利用率分别为 83.48%、79.59%,比0h时分别提高了23.56%、18.03%;TN、TP去除率分别提高了14.63%、16.98%.     

UF膜与混凝粉末活性炭联用处理微污染原水

采用混凝、粉末活性炭和UF膜分离的联用技术对黄浦江原水进行试验 ,结果表明 ,混凝、粉末活性炭可有效地去除溶解性有机物 .混凝处理主要去除大分子量的有机物 ,粉末活性炭主要去除低分子量的有机物 .混凝、粉末活性炭还能有效地去除三氯甲烷生成潜能 (THMFP) ,对于低分子量的THMFP ,混凝去除效果很差 ,而粉末活性炭去除很好 .试验还表明 ,混凝、粉末活性炭还可大大降低膜的滤饼层阻力 ,当混凝剂投加量为 4mg/L时 ,膜的滤饼层阻力最小 .     

Characteristics of molecular weight distribution of dissolved organic matter in bromide-containing water and disinfection by-product formation properties during treatment processes

The characteristics of dissolved organic matter (DOM) and bromide ion concentration have a significant influence on the formation of disinfection by-products (DBPs). In order to identify the main DBP precursors, DOM was divided into five fractions based on molecular weight (MW), trihalomethane formation potential and haloacetic acid formation potential were determined for fractions, and the change in contents of different fractions and total DBPs during treatment processes (pre-chlorination, coagulation, sand filtration, disinfection) were studied. Moreover, the relationship between bromide concentration and DBP generation characteristics in processes was also analyzed. The results showed that the main DBP precursors were the fraction with MW < 1 kDa and fraction with MW 3−10 kDa, and the DBP''s generation ability of lower molecular weight DOM (< 10 kDa) was higher than that of higher molecular weight DOM. During different processes, pre-chlorination and disinfection had limited effect on removing organics but could alter the MW distribution, and coagulation and filtration could effectively remove organics with higher MW. For DBPs, trihalomethanes (THMs) were mainly generated in pre-chlorination and disinfection, while haloacetic acids (HAAs) were mostly generated during pre-chlorination; coagulation and sand filtration had little effect on THMs but resulted in a slight removal of HAAs. In addition, the results of ANOVA tests suggested that molecular sizes and treatment processes have significant influence on DBP formation. With increasing bromide concentration, the brominated DBPs significantly increased, but the bromine incorporation factor in the processes was basically consistent at each concentration.     

Changes in different organic matter fractions during conventional treatment and advanced treatment

XAD-8 resin isolation of organic matter in water was used to divide organic matter into the hydrophobic and hydrophilic fractions. A pilot plant was used to investigate the change in both fractions during conventional and advanced treatment processes. The treatment of hydrophobic organics (HPO), rather than hydrophilic organicas (HPI), should carry greater emphasis due to HPO’s higher trihalomethane formation potential (THMFP) and haloacetic acid formation potential (HAAFP). The removal of hydrophobic matter and its transmission into hydrophilic matter reduced ultimate DBP yield during the disinfection process. The results showed that sand filtration, ozonation, and biological activated carbon (BAC) filtration had distinct influences on the removal of both organic fractions. Additionally, the combination of processes changed the organic fraction proportions present during treatment. The use of ozonation and BAC maximized organic matter removal e ciency, especially for the hydrophobic fraction. In sum, the combination of pre-ozonation, conventional treatment, and O3-BAC removed 48% of dissolved organic carbon (DOC), 60% of HPO, 30% of HPI, 63% of THMFP, and 85% of HAAFP. The use of conventional treatment and O3-BAC without pre-ozonation had a comparable performance, removing 51% of DOC, 56% of HPO, 45% of HPI, 61% of THMFP, and 72% of HAAFP. The e ectiveness of this analysis method indicated that resin isolation and fractionation should be standardized as an applicable test to help assess water treatment process e ciency.     

The migration and transformation of dissolved organic matter during the freezing processes of water

This study investigated the partitioning behavior of dissolved organic matter(DOM) in liquid and ice phases, as well as the changes in the optical properties and chlorine reactivity of DOM during the freezing processes of water. DOM was rejected from the ice phase and accumulated in the remaining liquid phase during water freezing. Moreover, the decrease in freezing temperature, as well as the increase in dissolved organic carbon(DOC)concentration of feed water, caused an increase in DOM captured in the ice phase. The ultraviolet-absorbing compounds, trihalomethane precursors, as well as fulvic acid- and humic acid-like fluorescent materials, were more liable to be to be rejected from the ice phase and were more easily retained in the unfrozen liquid phase during water freezing, as compared with organics(on average) that comprise DOC. In addition, it was also found a higher accumulation of these organics in the unfrozen liquid phase during water freezing at higher temperature. The freeze/thaw processes altered the quantity, optical properties, and chlorine reactivity of DOM. The decrease in ultraviolet light at 254 nm as well as the production of aromatic protein- and soluble microbial byproduct-like fluorescent materials in DOM due to freeze/thaw were consistently observed. On the other hand, the changes in DOC, trihalomethane formation potential, and fulvic acid- and humic acid-like fluorescence caused by freeze/thaw varied significantly between samples.     

融雪期城市河流中溶解性有机物的时空分布特征

以沈阳市新开河为研究对象,考察了河水中溶解性有机物(DOM)含量的月份变化,以及融雪期河水中DOM含量和特性的时空变化规律.利用XAD树脂将DOM分为5个部分:疏水性有机酸(HPO-A),疏水性中性有机物(HPO-N),过渡亲水性有机酸(TPI-A),过渡亲水性中性有机物(TPI-N)和亲水性有机物(HPI).结果表明,融雪期河水中的溶解性有机碳(DOC)浓度较高,HPO-N和TPI-N是融雪期河水中的主要DOM组分,并且DOM中的荧光物质主要为类芳香族蛋白质荧光物质和类腐植酸荧光物质.融雪期水体中的DOC、波长254nm处的紫外吸光度(UV-254)和三卤甲烷生成势(THMFP)呈先降低然后波动最后升高的变化趋势.特征紫外吸光度(SUVA)和三卤甲烷生成活性(STHMFP)与以上三者的变化规律相反.融雪期河水中的DOC受污水排放影响大,有排污口处的DOC含量明显大于其他区域.污水排放也使受纳水体中UV-254对THMFP的指示作用减弱.     

The migration and transformation of dissolved organic matter during the freezing processes of water

This study investigated the partitioning behavior of dissolved organic matter (DOM) in liquid and ice phases, as well as the changes in the optical properties and chlorine reactivity of DOM during the freezing processes of water. DOM was rejected from the ice phase and accumulated in the remaining liquid phase during water freezing. Moreover, the decrease in freezing temperature, as well as the increase in dissolved organic carbon (DOC) concentration of feed water, caused an increase in DOM captured in the ice phase. The ultraviolet-absorbing compounds, trihalomethane precursors, as well as fulvic acid- and humic acid-like fluorescent materials, were more liable to be to be rejected from the ice phase and were more easily retained in the unfrozen liquid phase during water freezing, as compared with organics (on average) that comprise DOC. In addition, it was also found a higher accumulation of these organics in the unfrozen liquid phase during water freezing at higher temperature. The freeze/thaw processes altered the quantity, optical properties, and chlorine reactivity of DOM. The decrease in ultraviolet light at 254 nm as well as the production of aromatic protein- and soluble microbial byproduct-like fluorescent materials in DOM due to freeze/thaw were consistently observed. On the other hand, the changes in DOC, trihalomethane formation potential, and fulvic acid- and humic acid-like fluorescence caused by freeze/thaw varied significantly between samples.     

Dissolved organic matter removal using magnetic anion exchange resin treatment on biological effluent of textile dyeing wastewater

This study investigated the removal of dissolved organic matter（DOM） from real dyeing bio-treatment effluents（DBEs） with the use of a novel magnetic anion exchange resin（NDMP）.DOMs in two typical DBEs were fractionized using DAX-8/XAD-4 resin and ultrafiltration membranes. The hydrophilic fractions and the low molecular weight（MW）（〈3 kDa） DOM fractions constituted a major portion（〉50%） of DOMs for the two effluents. The hydrophilic and low MW fractions of both effluents were the greatest contributors of specific UV254absorbance（SUVA254）,and the SUVA254 of DOM fractions decreased with hydrophobicity and MW. Two DBEs exhibited acute and chronic biotoxicities. Both acute and chronic toxicities of DOM fractions increased linearly with the increase of SUVA254 value. Kinetics of dissolved organic carbon（DOC） removal via NDMP treatment was performed by comparing it with that of particle active carbon（PAC）. Results indicated that the removal of DOC from DBEs via NDMP was 60%,whereas DOC removals by PAC were lower than 15%. Acidic organics could be significantly removed with the use of NDMP. DOM with large MW in DBE could be removed significantly by using the same means. Removal efficiency of NDMP for DOM decreased with the decrease of MW. Compared with PAC,NDMP could significantly reduce the acute and chronic bio-toxicities of DBEs. NaCl/NaOH mixture regenerants,with selected concentrations of 10% NaCl（m/m）/1%NaOH（m/m）,could improve desorption efficiency.     

Prediction of DOM removal of low specific UV absorbance surface waters using HPSEC combined with peak fitting

High performance size exclusion chromatography (HPSEC) is used in water quality research primarily to determine the molecular weight distribution of the dissolved organic matter (DOM), but by applying peak fitting to the chromatogram, this technique can also be used as a tool to model and predict DOM removal. Six low specific UV absorbance (SUVA) source waters were treated using coagulation with alum and both the source and treated water samples were analysed using HPSEC. By comparing the molecular weight profiles of the source and treated waters, it was established that several DOM components were not effectively removed by alum coagulation even after high dosage alum treatment. A peak-fitting technique was applied based on the concept of linking the character (molecular weight profile) of the recalcitrant organics in the treated water with those of the source water. This was then applied to predict DOM treatability by determining the areas of the peaks which were assigned to removable organics from the source water molecular weight profile after peak fitting, and this technique quantified the removable and non-removable organics. The prediction was compared with the actual dissolved organic carbon (DOC) removal determined from jar testing and showed good agreement, with variance between 2% and 10%. This confirmed that this prediction approach, which was originally developed for high SUVA waters, can also be applied successfully to predict DOC removal in low SUVA waters.     

强化混凝去除黄浦江水有机物的试验研究

强化混凝去除有机物的效果与水源的分子量分布特性有着密切的关系.由于黄浦江水中低分子量的溶解性有机物占多数,因此,强化混凝处理有机物效果有限.对于＜1k分子量区间的有机物.增加混凝剂投量可有效去除紫外吸光值(UV254),但去除溶解性有机碳(DOC)的效果很差.尽管增加混凝剂投量和降低pH都能有效地去除有机物,但决定强化混凝效果的主要因素是pH,去除黄浦江水有机物的最佳pH范围为6～5.     

河流不同分子量溶解性有机质对全氟化合物赋存形态的影响

目前有关水体全氟化合物(PFASs)赋存特征的研究主要集中于总溶解态,对溶解性有机质(DOM)结合态PFASs的研究较为匮乏,尤其忽视了不同分子量DOM对PFASs赋存形态的影响. 为阐明河流上覆水体不同分子量DOM对PFASs赋存形态的影响,本文以长江干支流为例,分析了河流上覆水体11种典型PFASs (C4~C12)的浓度及组成,研究了不同分子量DOM结合态PFASs的赋存特征. 结果表明:①长江上覆水体中PFASs的平均浓度为52.6 ng/L,其中全氟戊酸(PFPeA)和全氟己酸(PFHxA)是最主要的单体污染物;由于受点源污染的影响,武汉段PFASs总溶解浓度及其单体浓度均显著高于其他采样点. ②长江上覆水体中DOM的浓度范围为0.08~3.84 mg/L (以C计),将水体DOM按分子量分离为<1 kDa、1~3 kDa、3~5 kDa、5~10 kDa和>10 kDa五种组分,各采样点中<1 kDa的溶解性有机碳(DOC)浓度(1.56~3.84 mg/L)显著高于其他分子量的DOC浓度. ③对于所检出的PFASs,<1 kDa DOM结合态PFASs (含自由溶解态)的浓度亦显著高于其他分子量DOM结合态PFASs的浓度,且其占水体总溶解态PFASs的比例均在85%以上,说明水体DOM结合态PFASs具有较高的生物有效性. 研究显示,水体不同分子量DOM结合态PFASs的赋存特征存在差异,因此对水体PFASs进行生态风险评价时需综合考虑不同分子量DOM结合态的含量及其生物有效性.